DK159100B - PROCEDURE FOR PREPARING A LIQUID VIRAL VACCINE CONTAINING A STABILIZER AND STABILIZER THAT CAN BE USED IN SUCH A PROCEDURE - Google Patents
PROCEDURE FOR PREPARING A LIQUID VIRAL VACCINE CONTAINING A STABILIZER AND STABILIZER THAT CAN BE USED IN SUCH A PROCEDURE Download PDFInfo
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- DK159100B DK159100B DK455880A DK455880A DK159100B DK 159100 B DK159100 B DK 159100B DK 455880 A DK455880 A DK 455880A DK 455880 A DK455880 A DK 455880A DK 159100 B DK159100 B DK 159100B
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K39/00—Medicinal preparations containing antigens or antibodies
- A61K39/12—Viral antigens
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/06—Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite
- A61K47/16—Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite containing nitrogen, e.g. nitro-, nitroso-, azo-compounds, nitriles, cyanates
- A61K47/18—Amines; Amides; Ureas; Quaternary ammonium compounds; Amino acids; Oligopeptides having up to five amino acids
- A61K47/183—Amino acids, e.g. glycine, EDTA or aspartame
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/06—Organic compounds, e.g. natural or synthetic hydrocarbons, polyolefins, mineral oil, petrolatum or ozokerite
- A61K47/26—Carbohydrates, e.g. sugar alcohols, amino sugars, nucleic acids, mono-, di- or oligo-saccharides; Derivatives thereof, e.g. polysorbates, sorbitan fatty acid esters or glycyrrhizin
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K47/00—Medicinal preparations characterised by the non-active ingredients used, e.g. carriers or inert additives; Targeting or modifying agents chemically bound to the active ingredient
- A61K47/30—Macromolecular organic or inorganic compounds, e.g. inorganic polyphosphates
- A61K47/42—Proteins; Polypeptides; Degradation products thereof; Derivatives thereof, e.g. albumin, gelatin or zein
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0012—Galenical forms characterised by the site of application
- A61K9/0019—Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K39/00—Medicinal preparations containing antigens or antibodies
- A61K2039/51—Medicinal preparations containing antigens or antibodies comprising whole cells, viruses or DNA/RNA
- A61K2039/525—Virus
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N2760/00—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA ssRNA viruses negative-sense
- C12N2760/00011—Details
- C12N2760/18011—Paramyxoviridae
- C12N2760/18411—Morbillivirus, e.g. Measles virus, canine distemper
- C12N2760/18434—Use of virus or viral component as vaccine, e.g. live-attenuated or inactivated virus, VLP, viral protein
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/30—Against vector-borne diseases, e.g. mosquito-borne, fly-borne, tick-borne or waterborne diseases whose impact is exacerbated by climate change
Description
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Den foreliggende opfindelse angår en fremgangsmåde til fremstilling af en flydende viral vaccine og specielt en stabilisator til brug ved fremstilling af en sådan vaccine.The present invention relates to a method for producing a liquid viral vaccine and, in particular, to a stabilizer for use in the preparation of such a vaccine.
5 På grund af den verdensomspændende distribuering af vacciner og uensartede omgivelsestemperaturer har der været et behov for at stabilisere disse præparater til transport og anvendelse. Der har været anvendt adskillige stabiliseringsmetoder i den forgangne tid.5 Due to the worldwide distribution of vaccines and disparate ambient temperatures, there has been a need to stabilize these preparations for transport and use. Several stabilization methods have been used in the past.
10 a) Lave temperaturer (-10 til -70°C).10 a) Low temperatures (-10 to -70 ° C).
Behovet for faciliteter til opbevaring ved lav temperatur, hvilke faciliteter ikke altid er tilgængelige, begrænser den praktiske gennemførelse af denne foranstaltning.The need for low temperature storage facilities, which are not always available, limits the practical implementation of this measure.
b) Lyophilisering.b) Lyophilization.
15 Skønt ly ophili sering lider af den ulempe at være en kostbar foranstaltning, er lyophiliserede vacciner rimeligt stabile og opbevares ved 4 til 8°C, indtil de skal anvendes. Under denne opbevaringsperiode forringes vaccinerne imidlertid langsomt, indtil de efter ca. 12 til 24 måneders forløb ikke har 20 en tilstrækkelig titer til at give immunitet. Da den lyophi-liserede vaccine endvidere må rekonstitueres før anvendelse, taber det flydende rekonstituerede præparat styrke under henstand ved stuetemperatur. Dette kan resultere i utilstrækkelig titer til at give immunitet og resultere i svigtende 2 5 immuni seringsprogram.Although lyophilization suffers from the disadvantage of being a costly measure, lyophilized vaccines are reasonably stable and stored at 4 to 8 ° C until used. However, during this storage period, the vaccines slowly deteriorate until after approx. For 12 to 24 months, 20 does not have a sufficient titre to confer immunity. Furthermore, since the lyophilized vaccine must be reconstituted before use, the liquid reconstituted preparation loses potency at room temperature. This can result in insufficient titres to confer immunity and result in a failure of the immunization program.
c) Stabili satorer.(c) Stabilizers.
Stabilisatorer er kemiske forbindelser, der sættes til vaccine, og de anvendes sammen med enten opbevaring ved lav temperatur eller lyophilisering. Kemiske stabilisatorer, 30 f.eks. SPGA (en stabilisator beskrevet af Bovamick et al·.,Stabilizers are chemical compounds added to the vaccine and are used in conjunction with either low temperature storage or lyophilization. Chemical stabilizers, e.g. SPGA (a stabilizer described by Bovamick et al.,
J. Bact. 59:509-522 (1950)) og lignende, er beskrevet i den til teknikkens stade hørende litteratur.'Som beskrevet af· Bovarnick et al., indeholder 1 liter SPGA 0,218 MJ. Bact. 59: 509-522 (1950)) and the like are described in the prior art literature. As described by Bovarnick et al., 1 liter of SPGA contains 0.218 M
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2 saccharose (74,62 g), 0,00376 Μ KE^PO^ (0,52 g), 0,0071 M i^HPO^ (1,25 g), 0,0049 M kaliumglutamat (0,912 g) og 1 % serumalbumin (10 g). Der kendes forskellige modifikationer af SPGA i henseende til de angivne mængder 5 og bestanddele, og det er let for fagmanden at modificere denne stabilisator. Således erstattes kaliumglutamat ofte med natriumglutamat, mens de modificerede præparater stadig betegnes SPGA. US patentskrift nr. 3 783 098, der svarer til fransk patentskrift nr. 2 115 379, hen-10 viser f.eks. til en SPGA-stabilisator indeholdende mo- nonatriumglutamat i stedet for monokaliumglutamat (spalte 6, linje 5-11). I US patentskrift nr. 3 933 585 beskrives en SPGA-stabilisator, der pr. liter sterildestilleret vand indeholder 74,62 g saccharose, 0,45 g KI^PO^, 1,35 15 g I^HPO^, 0,956 g mononatrium-L-glutamat og 40 ml af en 25 %*s opløsning af albuminosol (humant albumin).2 sucrose (74.62 g), 0.00376 Μ KE ^ PO ^ (0.52 g), 0.0071 M i ^ HPO ^ (1.25 g), 0.0049 M potassium glutamate (0.912 g) and 1 % serum albumin (10 g). Various modifications of SPGA are known with respect to the indicated quantities 5 and constituents, and it is easy for those skilled in the art to modify this stabilizer. Thus, potassium glutamate is often replaced with sodium glutamate while the modified formulations are still referred to as SPGA. U.S. Patent No. 3,783,098, corresponding to French Patent No. 2,115,379, cites e.g. to an SPGA stabilizer containing monosodium glutamate instead of monocalcium glutamate (column 6, lines 5-11). U.S. Patent No. 3,933,585 discloses an SPGA stabilizer which, at liter of sterile distilled water contains 74.62 g of sucrose, 0.45 g of KI 2 PO 2, 1.35 15 g of 1 HPO 2, 0.956 g of monosodium L-glutamate and 40 ml of a 25% * solution of albuminosol (human albumin).
1 almindelighed indeholder en SPGA-stabilisator ca.In general, an SPGA stabilizer contains approx.
2 til ca. 10 % sukker, f.eks. saccharose, ca. 0,05 til ca. 0,3 % af et mono- eller dibasisk alkalimetalphos- 20 phatsalt eller en blanding af sådanne salte, f.eks.2 to approx. 10% sugar, e.g. sucrose, ca. 0.05 to approx. 0.3% of a mono- or dibasic alkali metal phosphate salt or a mixture of such salts, e.g.
KE^PO^, l^HPO^, Na^PO^ og/eller Na2HPO^, ca. 0,05 til ca. 0,2 % glutaminsyre-alkalimetalsalt, f.eks. natriumeller kaliumglutamat, og ca. 0,5 % til 2 % serumalbumin, f.eks. bovint serumalbumin eller humant albumin. Der 25 kan foretages forskellige udskiftninger af bestanddele i formuleringen af SPGA-stabilisatoren. F.eks. kan saccharose som beskrevet i US patentskrift nr. 3 783 098 (spalte 3, linje 59-61) helt eller delvist erstattes med et stivelseshydrolysat, f.eks. glucose eller dextran, 30 og albumin kan som beskrevet i henholdsvis US patentskrift nr. 3 783 098 (spalte 3, linje 8) og US patentskrift nr. 3 915 794 helt eller delvist erstattes med casein eller polyvinylpyrrolidon. Ingen af de hidtil kendte stabilisatorer, ej heller de, der er beskrevet i Chemical 35 Abstracts 8_0 (1974), 41031 f, US patentskrift nr.KE ^ PO ^, l ^ HPO ^, Na ^ PO ^, and / or Na2HPO ^, ca. 0.05 to approx. 0.2% glutamic acid alkali metal salt, e.g. sodium or potassium glutamate, and approx. 0.5% to 2% serum albumin, e.g. bovine serum albumin or human albumin. Various components substitutions can be made in the formulation of the SPGA stabilizer. Eg. For example, sucrose as described in U.S. Patent No. 3,783,098 (column 3, lines 59-61) may be partially or completely replaced with a starch hydrolyzate, e.g. glucose or dextran, 30 and albumin can be replaced, in whole or in part, with casein or polyvinylpyrrolidone, as described in U.S. Patent No. 3,783,098 (column 3, line 8) and U.S. Patent No. 3,915,794, respectively. None of the prior art stabilizers, nor those described in Chemical 35 Abstracts 8_0 (1974), 41031 f., U.S. Pat.
4 147 772, og belgisk patentskrift nr. 665076 34,147,772, and Belgian Patent No. 665076 3
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indeholder både L-arginin og mononatriumglutamat eller glutaminsyre. Disse stabilisatorer er derfor ikke vedvarende stabile.contains both L-arginine and monosodium glutamate or glutamic acid. These stabilizers are therefore not permanently stable.
Det tilsigtes derfor med den foreliggende opfindelse 5 at tilvejebringe en forbedret fremgangsmåde til fremstilling af en flydende vaccine, ved hvilken man blander et inaktiveret eller svækket virus og en stabilisator i det væsentlige bestående af 1,5 til 2,1 vægtdele delvist hydrolyseret gelatine med en molvægt på ca. 3000, 10 7,0 til 13,0 vægtdele monosaccharid, disaccharid eller sorbitol, 0,4 til 0,6 vægtdele af et in vitro celledyrkningsmedium og en sådan mængde af en fysiologisk acceptabel sur puffer, som er i stand til at holde pH på 6,0 til 6,5.It is therefore an object of the present invention to provide an improved method for preparing a liquid vaccine by mixing an inactivated or attenuated virus and a stabilizer consisting essentially of 1.5 to 2.1 parts by weight of partially hydrolyzed gelatin with a molar weight of approx. 3000, 10 7.0 to 13.0 parts by weight of monosaccharide, disaccharide or sorbitol, 0.4 to 0.6 parts by weight of an in vitro cell culture medium, and such amount of a physiologically acceptable acid buffer capable of maintaining pH of 6.0 to 6.5.
15 Fremgangsmåden ifølge opfindelsen er ejendommelig ved, T- at stabilisatoren indeholder 0,35 til 0,7 vægtdele L- glutaminsyre og 0,75 til 1,3 vægtdele L-arginin.The process according to the invention is characterized in that the stabilizer contains 0.35 to 0.7 parts by weight of L-glutamic acid and 0.75 to 1.3 parts by weight of L-arginine.
Opfindelsen angår som nævnt også en stabilisator til brug ved fremstilling af en flydende vaccine, som oven-20 for nævnt, hvilken stabilisator i alt væsentligt består af 1,5 til 2,1 vægtdele delvist hydrolyseret gelatine med en molvægt på ca. 3000, 7,0 til 13,0 vægtdele monosaccharid, disaccharid eller sorbitol, ca. 0,4 til 0,6 vægtdele af et in vitro celledyrkningsmedium og 25 en sådan mængde fysiologisk acceptabel sur puffer, som er effektiv til at indstille pH på 6,0 til 6,5.The invention also relates, as mentioned, to a stabilizer for use in the preparation of a liquid vaccine, as mentioned above, which essentially consists of 1.5 to 2.1 parts by weight of partially hydrolyzed gelatin having a mole weight of approx. 3000, 7.0 to 13.0 parts by weight of monosaccharide, disaccharide or sorbitol, ca. 0.4 to 0.6 parts by weight of an in vitro cell culture medium and such amount of physiologically acceptable acidic buffer effective to adjust the pH of 6.0 to 6.5.
Stabilisatoren ifølge opfindelsen er ejendommelig ved, at den også indeholder 0,35 til 0,7 vægtdele L-glutamin-syre og 0,75 til 1,3 vægtdele L-arginin.The stabilizer of the invention is characterized in that it also contains 0.35 to 0.7 parts by weight of L-glutamic acid and 0.75 to 1.3 parts by weight of L-arginine.
30 En sådan stabilisator giver en forøget, vedvarende stabilitet, som ingen af de kendte stabilisatorer udviser.Such a stabilizer provides increased sustained stability which none of the known stabilizers exhibit.
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Den flydende vaccine kan opnås ved at optø en frossen vaccine eller ved at rekonstituere en lyophiliseret vaccine. Eksempler på levende vira er mæslinger, fåresyge, røde hunde, skoldkopper, polio og hepatitis eller 5 en kombination af to eller flere af de nævnte vira.The liquid vaccine can be obtained by thawing a frozen vaccine or by reconstituting a lyophilized vaccine. Examples of live viruses are measles, mumps, rubella, chickenpox, polio and hepatitis, or a combination of two or more of the viruses mentioned.
Hydrolyseret gelatine anvendes for at opnå en opløselig, ikke-gelerende proteinmatrix med ringe eller ingen pyro-genicitet eller antigenicitet.Hydrolyzed gelatin is used to obtain a soluble, non-gelling protein matrix with little or no pyrogenicity or antigenicity.
Ved delvist hydrolyseret gelatine forstås gelatine, der er 10 blevet underkastet en ,delvis hydrolyse til opnåelse af delvist hydrolyseret gelatine med en molekylvægt på ca. 3000. Dette gelatinehydrolyseprodukt har tilnærmelsesvis samme amino syre sammensætning som gelatine. Ulig gelatine, som danner geler, men er uopløselig i koldt vand, danner hy-15 drolyseret gelatine ikke gel, men er opløselig i koldt vand og andre almindelige væsker, såsom mælk og orangejuice. Vandige opløsninger indeholdende op til ca. 10% hydrolyseret gelatine forøger ikke viskositeten i nævneværdig grad.By partially hydrolyzed gelatin is meant gelatin which has been subjected to a partial hydrolysis to obtain partially hydrolyzed gelatin having a molecular weight of approx. 3000. This gelatin hydrolysis product has approximately the same amino acid composition as gelatin. Unlike gelatin which forms gels but is insoluble in cold water, hydrolyzed gelatin does not form gel but is soluble in cold water and other common liquids such as milk and orange juice. Aqueous solutions containing up to approx. 10% hydrolyzed gelatin does not significantly increase viscosity.
Ved over ca. 10%'s koncentration forøges viskositeten langsomt. 20 Ved ca. 50%’s koncentration er opløsningerne ret viskose.At over approx. 10% concentration increases viscosity slowly. 20 At approx. At 50% concentration, the solutions are quite viscous.
Den typiske amino syre sammensætning for hydrolyseret gelatine er som følger:The typical amino acid composition for hydrolyzed gelatin is as follows:
Alanin 8,5 %Alanine 8.5%
Arginin 7 > 9 % 25 Aspartinsyre 5,7 %Arginine 7> 9% Aspartic acid 5.7%
Cystin 0,08 %Cystine 0.08%
Glutaminsyre 9,5 %Glutamic Acid 9.5%
Glycin 22,8 %Glycine 22.8%
Histidin 0,77 % 30 Hydroxyprolin 13-14 %Histidine 0.77% Hydroxyproline 13-14%
Isoleucin 1,3 %Isoleucine 1.3%
Leucin 2,9 %Leucine 2.9%
Lysin 4,2 %Lysine 4.2%
Methionin 0,78% 35 Phenylalanin 2,0 %Methionine 0.78% Phenylalanine 2.0%
Prolin 13,8 % 5Proline 13.8% 5
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Serin 3,3 %Serine 3.3%
Threonin 1,9 %Threonine 1.9%
Tyrosin 0,40 %Tyrosine 0.40%
Valin 2,4 % 5 Delvist hydrolyseret gelatine kan opnås ved enzymatisk hydrolyse af gelatine ved hjælp af et proteolytisk enzym, såsom papain, chymopapain og bromelin, skønt andre kendte hydrolysemidler kan anvendes, f.eks. sur hydrolyse. Passende hydrolyseret gelatine opnås fra Wilson and Co., Inc., 10 Calumet City, Illinois under handelsnavnet SOL-U-PRO.Valine 2.4% Partially hydrolyzed gelatin can be obtained by enzymatic hydrolysis of gelatin by a proteolytic enzyme such as papain, chymopapain and bromelain, although other known hydrolysing agents may be used, e.g. acid hydrolysis. Appropriate hydrolyzed gelatin is obtained from Wilson and Co., Inc., 10 Calumet City, Illinois under the trade name SOL-U-PRO.
Stabilisatoren indeholder også et monosaccharid, f.eks. sorbitol, eller et disaccharid, f.eks. saccharose, lactose eller maltose. Saccharose foretrækkes.The stabilizer also contains a monosaccharide, e.g. sorbitol, or a disaccharide, e.g. sucrose, lactose or maltose. Sucrose is preferred.
L-glutaminsyren kan anvendes som sådan eller i form af sit 15 . natriumsalt, mononatriumglutamat.The L-glutamic acid can be used as such or in the form of its 15. sodium salt, monosodium glutamate.
L-argininen kan anvendes som sådan eller i form af hydro-chloridet.The L-arginine can be used as such or in the form of the hydrochloride.
Den sure puffer kan være en vilkårlig fysiologisk acceptabel puffer, som opretholder det ønskede pH på 6 til 20 6,5, f.eks. en phosphatpuffer, acetatpuffer eller citrat puffer. En phosphatpuffer foretrækkes. Stabilisatoren fortyndes med fra 3 til 8 gange, foretrukkent ca. 5,5 crange, sin egen vægt destilleret vand før anvendelse.The acidic buffer may be any physiologically acceptable buffer which maintains the desired pH of 6 to 6.5, e.g. a phosphate buffer, acetate buffer or citrate buffer. A phosphate buffer is preferred. The stabilizer is diluted from 3 to 8 times, preferably approx. 5.5 crange, its own weight of distilled water before use.
Ved et celledyrkningsmedium forstås et næringsmedium, der 25 muliggør vækst af celler in vitro. Specielle næringsmedier er f.eks. Medium 199, Morgan et al., Proc. Soc. Exp. Biol.A cell culture medium is understood to mean a nutrient medium that enables cell growth in vitro. Special nutritional media are e.g. Medium 199, Morgan et al., Proc. Soc. Exp. Biol.
& Med., 73:1-8, 1950; Basal Medium Eagle, Eagle, Science, 122, 501-504, 1955; In Vitro, bind 6, nr. 2, 1970; Dul-becco’s Modified Eagle’s Medium, Dulbecco et al., Virology, 30 8, 396, 1959; Smith et al., J. Virol., 12, 185-196, I960;& Med., 73: 1-8, 1950; Basal Medium Eagle, Eagle, Science, 122, 501-504, 1955; In Vitro, Volume 6, No. 2, 1970; Dul-becco's Modified Eagle's Medium, Dulbecco et al., Virology, 30 8, 396, 1959; Smith et al., J. Virol., 12, 185-196, I960;
In Vitro, bind 6, nr. 2, 1970; Minimum Essential Medium (Eagle), Science, 130, 432 (1959) og RPMI Media, Moore et al., 199, 519-524, 1967; In Vitro, bind 6, nr. 2, 1970.In Vitro, Volume 6, No. 2, 1970; Minimum Essential Medium (Eagle), Science, 130, 432 (1959) and RPMI Media, Moore et al., 199, 519-524, 1967; In Vitro, Volume 6, No. 2, 1970.
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Stabilisatoren ifølge opfindelsen kan anvendes til fremstilling af forskellige flydende virale vacciner, som f.eks. vacciner mod mæslinger, fåresyge, røde hunde, respiratorisk syncytialvirus, parainfluenza type 1, 5 2 og 3 og cytomegalovirus.The stabilizer according to the invention can be used for the preparation of various liquid viral vaccines, e.g. vaccines against measles, mumps, rubella, respiratory syncytial virus, parainfluenza types 1, 5 2 and 3 and cytomegalovirus.
Sammensætningen af stabilisatoren ifølge opfindelsen kan f.eks. være som følger:The composition of the stabilizer according to the invention can e.g. be as follows:
Bestanddel Vægtdele/50 ml 10 Delvist hydrolyseret gelatine 1,5 - 2,1Ingredient Weight parts / 50 ml 10 Partially hydrolyzed gelatin 1.5 - 2.1
Mono- eller disaccharid 7,0 -13,0 Næringsmedium (fast stof) 0,4 - 0,6 L-glutaminsyre 0,35- 0,7 L-arginin 0,75- 1,3 15 Fysiologisk acceptabel puffer til indstilling af pH til 6,0Mono- or disaccharide 7.0 -13.0 Nutrient medium (solid) 0.4 - 0.6 L-glutamic acid 0.35- 0.7 L-arginine 0.75-1.3 Physiologically acceptable buffer to adjust pH to 6.0
til 6,5 0,05- 0,2 Mto 6.5 0.05 to 0.2 M
Særligt foretrukne formuleringer for stabilisatoren til den flydende virale vaccine som omhandlet i den foreliggende opfindelse er som følger: 20Particularly preferred formulations for the liquid viral vaccine stabilizer as contemplated by the present invention are as follows:
Delvist hydrolyseret gelatine y}g gPartially hydrolyzed gelatin y} g g
Saccharose eller sorbitol 10,0 gSucrose or sorbitol 10.0 g
Medium 199 0,55 gMedium 199 0.55 g
Mononatriumglutamat 0,5 g L-arginin-HCl 1,0 g 2 5Monosodium glutamate 0.5 g L-arginine HCl 1.0 g 2.5
Natrium pho sphatpuf f er 1 M, pH 6,2 5 mlSodium pho sphatpuf f is 1 M, pH 6.2 5 ml
Vand til 50,0 mlWater to 50.0 ml
Stabilisatoren kan desuden indeholde, og indeholder forego trukkent, en lille smule NaHCO^ og phenolrødt. I et præparat som det i det foregående angivne kan NaHCO^ være til stede i en mængde på ca. 1,2 g og phenolrødt i en mængde på ca. 0,01 g. Skønt særlige præparater er beskrevet i detIn addition, the stabilizer may contain, and contains forego, a small amount of NaHCO 3 and phenol red. In a composition such as the one described above, NaHCO 3 may be present in an amount of approx. 1.2 g and phenol red in an amount of approx. 0.01 g. Although special preparations are described in it
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7 foregående vil det forstås, at forhold og koncentrationer for hver enkelt bestanddel kan varieres. Et volumen massevaccine fortyndes sædvanligvis med ca. 2 til ca. 12 volumina stabilisator.7 above, it will be understood that the ratios and concentrations of each component may be varied. A volume of mass vaccine is usually diluted by approx. 2 to approx. 12 volume stabilizer.
5 De efterfølgende eksempler forklarer den foreliggende opfindelse nærmere.The following examples further explain the present invention.
Eksempel 1 40 ml mæslingeviruskoncentrat, som er blevet opbevaret ved -70°C, optøs i et vandbad ved 25° C og holdes derpå ved 4 -10 8°C. Det flydende viruskoncentrat opdeles i to alikvoter på hver 16,5 ml.Example 1 40 ml of measles virus concentrate, which has been stored at -70 ° C, is thawed in a water bath at 25 ° C and then kept at 4 -10 8 ° C. The liquid virus concentrate is divided into two aliquots of 16.5 ml each.
A) En alikvot på 16,5 ml af denne virusvæske fortyndes med 50 ml af følgende stabilisator, der er steriliseret ved passage gennem en 0,2 y-um membran.A) An aliquot of 16.5 ml of this viral fluid is diluted with 50 ml of the following stabilizer, which is sterilized by passage through a 0.2 µm membrane.
15 1 M phosphatpuffer, pH 6,2 5,0 ml15 M phosphate buffer, pH 6.2 5.0 ml
Sorbitol, 25%’s vandig opløsning 7,1 mlSorbitol, 25% aqueous solution 7.1 ml
Hydrolyseret gelatine, 25%ts vandig opløsning 7,1 mlHydrolyzed gelatin, 25% ts aqueous solution 7.1 ml
Medium 199 30,7 mlMedium 199 30.7 ml
Formulering udføres under aseptiske betingelser og laminar strømningshætte. For at undgå mikrobiel vækst sættes neomycin (0,1 ml, 2500 enheder) til præparatet. Den fortyndede vaccine anbringes i 2 ml glasampuller (0,7 ml vaccine pr. ampul), som straks flammelukkes og opbevares ved 37°C.Formulation is performed under aseptic conditions and laminar flow cap. To avoid microbial growth, add neomycin (0.1 ml, 2500 units) to the preparation. The diluted vaccine is placed in 2 ml vials (0.7 ml vaccine per ampoule), which are immediately flame-sealed and stored at 37 ° C.
B) Den anden alikvot på 16,5 ml behandles som den første med den undtagelse, at stabilisatorpræparatet yderligere indeholder 0,5 g mononatriumglutamat, 1,0 g L-arginin-HCl og 10 g saccharose i stedet for sorbitol.B) The second aliquot of 16.5 ml is treated as the first except that the stabilizer preparation further contains 0.5 g monosodium glutamate, 1.0 g L-arginine HCl and 10 g sucrose instead of sorbitol.
DK 159100 BDK 159100 B
88
Opbevaringsstabilitet for vaccinerne fremgår af efterfølgen-- de tabel:Storage stability of the vaccines is shown in the following table:
Titere ^ af flydende vacciner opbevaret ved 37°CTiters ^ of liquid vaccines stored at 37 ° C
5 Tid, Stabilisator med Stabilisator med5 Time, Stabilizer with Stabilizer with
timer formulering A formulering Bhours formulation A formulation B
O 3,9 3,7 24 2,3 3,1 48 2,0 2,7 10 72 1,5 2,5 ^ titere er udtrykt som TCID^q/0,1 ml.O 3.9 3.7 24 2.3 3.1 48 2.0 2.7 10 72 1.5 2.5 ^ titers are expressed as TCID ^ q / 0.1 ml.
Eksempel 2 25 ml mæslingeviruskoncentrat, som er blevet opbevaret ved -70°C, optøs i et vandbad ved 25°C og holdes derpå ved 4 -8°C. Det flydende virale koncentrat fortyndes med 75 ml stabilisator B (eks. 1) og anbringes i 2 ml glasampuller. Ampullerne varmforsegles og opbevares ved 2 - 8°C. Opbevaringsstabiliteten for vaccinen beskrives i følgende tabel:Example 2 25 ml of measles virus concentrate, which has been stored at -70 ° C, is thawed in a water bath at 25 ° C and then kept at 4 -8 ° C. The liquid viral concentrate is diluted with 75 ml of Stabilizer B (Example 1) and placed in 2 ml vials. The ampoules are heat sealed and stored at 2 - 8 ° C. The storage stability of the vaccine is described in the following table:
Stabilitet for flydende vaccine opbevaret ved 2 - 8°CStability of liquid vaccine stored at 2 - 8 ° C
2020
Tid, måneder Titer (TCIDr-0/0,l ml) 0 3,7 1 4,1 l 3,1 £ 3,5 25 ® 3,3Time, months Titer (TCIDr-0 / 0.1 ml) 0 3.7 1 4.1 l 3.1 £ 3.5 25 ® 3.3
Eksempel 3Example 3
Den efterfølgende tabel sammenligner stabiliteten for 4 potioner flydende mæslingevaccine fremstillet på forskellige tidspunkter under anvendelse af stabilisatorer med sammen-30 sætning A eller B som beskrevet i eks. 1.The following table compares the stability of 4 potions of liquid measles vaccine prepared at various times using stabilizers of composition A or B as described in Example 1.
DK 159100 BDK 159100 B
99
Titer (TCID50/0,1 ml) efter det angivne antal timer Portion Stabilisator _ ved 37°C_ O 24 48 72 5 1 A 3,9 2,3 2,0 1,5 1 B 3,7 3,1 2,7 2,5 2 A 4,0 3,1 2,5 1,8 2 B 3,9 3,6 3,0 2,6 3 A 3,9 — 2,2 2,1 10 3 B 3,6 3,3 3,0 2,5 4 A 3,5 2,1 1,6 1,5 4 B 3,'6 - - 3,5 - ' - 3,1 2,4Titre (TCID 50 / 0.1 ml) after the specified number of hours Stabilizer _ at 37 ° C_ 0 24 48 72 5 1 A 3.9 2.3 2.0 1.5 1 B 3.7 3.1 2, 7 2.5 2 A 4.0 3.1 2.5 1.8 2 B 3.9 3.6 3.0 2.6 3 A 3.9 - 2.2 2.1 10 3 B 3.6 3.3 3.0 2.5 4 A 3.5 2.1 1.6 1.5 4 B 3, '6 - - 3.5 -' - 3.1 2.4
Claims (10)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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US8906879A | 1979-10-29 | 1979-10-29 | |
US8906879 | 1979-10-29 | ||
US11870380A | 1980-02-05 | 1980-02-05 | |
US11870380 | 1980-02-05 |
Publications (3)
Publication Number | Publication Date |
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DK455880A DK455880A (en) | 1981-04-30 |
DK159100B true DK159100B (en) | 1990-09-03 |
DK159100C DK159100C (en) | 1991-02-11 |
Family
ID=26780218
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK455880A DK159100C (en) | 1979-10-29 | 1980-10-28 | PROCEDURE FOR PREPARING A LIQUID VIRAL VACCINE CONTAINING A STABILIZER AND STABILIZER THAT CAN BE USED IN SUCH A PROCEDURE |
Country Status (7)
Country | Link |
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EP (1) | EP0028563B1 (en) |
DE (1) | DE3067376D1 (en) |
DK (1) | DK159100C (en) |
ES (1) | ES496358A0 (en) |
GR (1) | GR70319B (en) |
IE (1) | IE50276B1 (en) |
PT (1) | PT71926B (en) |
Families Citing this family (33)
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JPS5716823A (en) * | 1980-07-03 | 1982-01-28 | Green Cross Corp:The | Live mumps vaccine pharmaceutical and stabilizing method |
US4554101A (en) * | 1981-01-09 | 1985-11-19 | New York Blood Center, Inc. | Identification and preparation of epitopes on antigens and allergens on the basis of hydrophilicity |
CA1206094A (en) * | 1981-01-09 | 1986-06-17 | Thomas P. Hopp | Synthetic antigenic composition and process for making same |
FR2505657A1 (en) * | 1981-05-13 | 1982-11-19 | Pasteur Institut | IMPROVEMENTS IN LIVE STABILIZING AGENTS FOR THE PREPARATION OF VACCINES, AND STABILIZED VACCINES CONTAINING SAID STABILIZING AGENTS |
FR2532548B1 (en) * | 1982-09-03 | 1985-11-08 | Pasteur Institut | NOVEL PROCESS FOR THE PRODUCTION OF VACCINES HAVING A HIGH TITLE OF VIRUSES AND HIGHLY PURIFIED VACCINES, A HIGH TITLE OF VIRUSES, SO OBTAINED |
JPS6314729A (en) * | 1986-06-30 | 1988-01-21 | スミスクライン・バイオロジカルス・ソシエテ・アノニム | Improved stabilizer for live vaccine, manufacture and vaccine containing same |
JPS63307827A (en) * | 1987-06-08 | 1988-12-15 | Kitasato Inst:The | Stabilized live vaccine and production thereof |
AU1633092A (en) * | 1991-05-17 | 1992-11-19 | Merck & Co., Inc. | Non-stinging vaccine composition |
CA2075521C (en) * | 1992-05-05 | 1995-11-28 | Kuniaki Koyama | Stabilized live vaccine |
US6403098B1 (en) * | 1996-09-26 | 2002-06-11 | Merck & Co., Inc. | Rotavirus vaccine formulations |
AU725231B2 (en) * | 1996-12-20 | 2000-10-12 | Merck & Co., Inc. | Stabilisers for lyophilised vaccines |
US6051238A (en) * | 1996-12-20 | 2000-04-18 | Merck & Co., Inc. | Stabilizers for lyophilized mumps vaccines |
GB9808922D0 (en) * | 1998-04-24 | 1998-06-24 | Cantab Pharmaceuticals Res Ltd | Virus preparations |
EP1305043A2 (en) * | 2000-07-31 | 2003-05-02 | Aventis Pasteur Limited | Respiratory syncytial virus vaccine |
US7914979B2 (en) * | 2004-11-05 | 2011-03-29 | Wellstat Biologics Corporation | Stable and filterable enveloped virus formulations |
US20060141483A1 (en) * | 2004-12-23 | 2006-06-29 | Calton Gary J | Stabilization of viral compositions |
US8097245B2 (en) | 2005-12-28 | 2012-01-17 | Advanced Bionutrition Corporation | Delivery vehicle for probiotic bacteria comprising a dry matrix of polysaccharides, saccharides and polyols in a glass form and methods of making same |
US8460726B2 (en) | 2006-12-18 | 2013-06-11 | Advanced Bionutrition Corporation | Dry food product containing live probiotic |
CA2756883C (en) | 2009-03-27 | 2018-01-09 | Advanced Bionutrition Corp. | Microparticulated vaccines for the oral or nasal vaccination and boostering of animals including fish |
MX2011012586A (en) | 2009-05-26 | 2012-03-26 | Advanced Bionutrition Corp | Stable dry powder composition comprising biologically active microorganisms and/or bioactive materials and methods of making. |
US9504750B2 (en) | 2010-01-28 | 2016-11-29 | Advanced Bionutrition Corporation | Stabilizing composition for biological materials |
RU2535869C2 (en) | 2010-01-28 | 2014-12-20 | Эдванст Бионутришн Корпорейшн | Dry glass-like composition for stabilisation and protection of biologically active material, and method for its obtaining |
CN103140145B (en) | 2010-08-13 | 2014-08-20 | 高级生物营养公司 | Dry storage stabilizing composition for biological materials |
ES2765880T3 (en) | 2012-01-09 | 2020-06-11 | Sanofi Pasteur Biologics Llc | Herpes virus purification |
US11260123B2 (en) | 2012-05-21 | 2022-03-01 | Sanofi Pasteur Limited | Herpesvirus compositions and related methods |
US9314519B2 (en) | 2012-08-21 | 2016-04-19 | Intervet Inc. | Liquid stable virus vaccines |
US9393298B2 (en) | 2013-03-15 | 2016-07-19 | Intervet Inc. | Liquid stable bovine virus vaccines |
US9480739B2 (en) | 2013-03-15 | 2016-11-01 | Intervet Inc. | Bovine virus vaccines that are liquid stable |
AR097762A1 (en) | 2013-09-27 | 2016-04-13 | Intervet Int Bv | DRY FORMULATIONS OF VACCINES THAT ARE STABLE AT ENVIRONMENTAL TEMPERATURE |
AR099470A1 (en) | 2014-02-17 | 2016-07-27 | Intervet Int Bv | LIQUID CORRAL BIRD VIRUS VACCINES |
TWI670085B (en) * | 2014-02-19 | 2019-09-01 | 荷蘭商英特威國際公司 | Swine virus vaccines that are liquid stable |
AU2016297986B8 (en) | 2015-07-29 | 2020-06-11 | Advanced Bionutrition Corp. | Stable dry probiotic compositions for special dietary uses |
WO2020251843A1 (en) * | 2019-06-10 | 2020-12-17 | Boehringer Ingelheim Animal Health USA Inc. | Stabilized liquid live vaccine |
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BE641705A (en) * | 1963-12-23 | 1964-06-23 | ||
BE665076A (en) * | 1963-12-23 | 1965-12-08 | ||
FR2076787A5 (en) * | 1970-01-28 | 1971-10-15 | Merieux Inst | Lyophilisation stabiliser - for viruses contg potassium phosphate lactose and albumin |
NL7115348A (en) * | 1970-11-25 | 1972-05-29 | ||
US3783098A (en) * | 1971-08-10 | 1974-01-01 | Cornell Res Foundation Inc | Highly potent,viable and stable cellfree virus preparations from cells infected with cell-associated viruses and method for obtaining the same |
IL44143A0 (en) * | 1973-02-07 | 1974-05-16 | Wellcome Found | Method of inactivating viruses and vaccines prepared thereby |
US3915794A (en) * | 1973-02-09 | 1975-10-28 | Rit Rech Ind Therapeut | Stabilizing compositions for cell-free viruses and cell-free virus preparations containing them |
US4147772A (en) * | 1976-02-03 | 1979-04-03 | Merck & Co., Inc. | Vaccine stabilizer |
DE2816349A1 (en) * | 1978-04-14 | 1979-10-25 | Merck & Co Inc | Preservatives for vaccines - contg. hydrolysed gelatin, sorbitol, culture medium and a buffer at pH 6-6.5 |
FR2424031A1 (en) * | 1978-04-24 | 1979-11-23 | Merck & Co Inc | Preservatives for vaccines - contg. hydrolysed gelatin, sorbitol, culture medium and a buffer at pH 6-6.5 |
BE866330A (en) * | 1978-04-25 | 1978-10-25 | Merck & Co Inc | METHOD OF MANUFACTURING A VACCINE STABILIZATION AGENT |
LU79529A1 (en) * | 1978-04-26 | 1978-11-28 | Merck & Co Inc | METHOD OF MANUFACTURING A VACCINE STABILIZATION AGENT |
-
1980
- 1980-10-16 PT PT71926A patent/PT71926B/en unknown
- 1980-10-17 GR GR63176A patent/GR70319B/el unknown
- 1980-10-28 DE DE8080401527T patent/DE3067376D1/en not_active Expired
- 1980-10-28 IE IE2225/80A patent/IE50276B1/en not_active IP Right Cessation
- 1980-10-28 ES ES496358A patent/ES496358A0/en active Granted
- 1980-10-28 EP EP80401527A patent/EP0028563B1/en not_active Expired
- 1980-10-28 DK DK455880A patent/DK159100C/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
DK455880A (en) | 1981-04-30 |
DE3067376D1 (en) | 1984-05-10 |
ES8202584A1 (en) | 1982-02-01 |
DK159100C (en) | 1991-02-11 |
EP0028563B1 (en) | 1984-04-04 |
EP0028563A1 (en) | 1981-05-13 |
PT71926B (en) | 1982-03-31 |
IE802225L (en) | 1981-04-29 |
IE50276B1 (en) | 1986-03-19 |
PT71926A (en) | 1980-11-01 |
GR70319B (en) | 1982-09-10 |
ES496358A0 (en) | 1982-02-01 |
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